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    MULTI-TUBE FIXED-BED REACTOR, ESPECIALLY FOR CATALYTIC GAS PHASE REACTIONS
    4.
    发明申请
    MULTI-TUBE FIXED-BED REACTOR, ESPECIALLY FOR CATALYTIC GAS PHASE REACTIONS 审中-公开
    管式反应器，尤其气相催化反应的

    公开(公告)号：WO0054877A3

    公开(公告)日：2001-04-05

    申请号：PCT/EP0002304

    申请日：2000-03-15

    Applicant: BASF AG ,  OLBERT GERHARD ,  CORR FRANZ ,  REUTER PETER ,  WAMBACH LUDWIG ,  HAMMON ULRICH

    Inventor： OLBERT GERHARD ,  CORR FRANZ ,  REUTER PETER ,  WAMBACH LUDWIG ,  HAMMON ULRICH

    IPC: B01J8/06 ,  B01J19/00 ,  B01J19/24 ,  C07C45/35 ,  C07C45/38

    CPC classification number: C07C45/35 ,  B01J8/067 ,  B01J19/0013 ,  B01J19/2425 ,  B01J2208/00212 ,  B01J2208/00221 ,  B01J2208/00256 ,  B01J2219/00094 ,  B01J2219/00103 ,  C07C45/38 ,  C07C47/22 ,  C07C47/127

    Abstract: The invention relates to a multi-tube fixed-bed reactor and to the use of a reactor of this type for carrying out catalytic gas phase reactions, especially for carrying out exothermic or endothermic catalytic gas phase reactions such as producing phthalic anhydride (PSA), acrylic acid (AA), methacrylic acid (MAA), acrolein, maleic anhydride (MSA), glyoxal, phosgene, hydrogen cyanide or vinyl formamide (VFA). According to the invention, in the case of larger reactors where a considerable reaction heat is produced or required and must be dissipated as a result of the numerous reaction tubes (17), the ratio of tube distribution t to tube outer diameter d?a? is made dependant on the reactor diameter or the tube bundle diameter d?RBa?. If the outer diameter of the reaction tube bundle (18) is more than 4 metres, a ratio of tube distribution t to tube outer diameter d?a? of at least 1.3 is preferred.

    Abstract translation: 本发明涉及一种管束反应器和用于进行气相催化反应，特别是用于进行放热或吸热催化气相反应如生产Phthalsälureanhydrid（PSA），丙烯酸（AA），甲基丙烯酸（MAA），丙烯醛，马来酸酐的使用这样的反应器中的（ MSA），乙二醛，光气，氢氰酸或乙烯基甲酰胺（VFA）。 根据本发明，在较大的反应器，其中，这是因为许多反应管（17）的已被获得的反应的高的热或需要，管间距的比率管外径d·A· 在反应器直径或管束外径d？RBA？ 让他们依赖。 具有大于4米反应管束（18）的外直径，管间距吨到管外径d的比·A· 优选为至少1.3。

    COUNTERFLOW REACTOR WITH A BUNDLE OF CONTACT TUBES
    6.
    发明申请
    COUNTERFLOW REACTOR WITH A BUNDLE OF CONTACT TUBES 审中-公开
    与联系人管逆流反应器

    公开(公告)号：WO0187476A8

    公开(公告)日：2001-12-13

    申请号：PCT/EP0104975

    申请日：2001-05-03

    Applicant: BASF AG ,  OLBERT GERHARD ,  CORR FRANZ

    Inventor： OLBERT GERHARD ,  CORR FRANZ

    IPC: C07D307/60 ,  B01J19/00 ,  B01J19/24 ,  C07C45/35 ,  C07C47/127 ,  C07C47/22 ,  C07C51/215 ,  C07C51/25 ,  C07C51/265 ,  C07C57/04 ,  C07C57/05 ,  C07D307/89 ,  F28F27/02 ,  C07D401/06 ,  C07D401/12 ,  C07D401/14 ,  C07D405/14

    CPC classification number: C07C51/252 ,  B01J19/0013 ,  B01J19/2425 ,  B01J2219/00094 ,  B01J2219/00103 ,  C07C45/35 ,  C07C47/127 ,  C07C51/215 ,  C07C51/265 ,  F28F27/02 ,  C07C47/22 ,  C07C57/145 ,  C07C57/04 ,  C07C63/16

    Abstract: The invention relates to a reactor (1) comprising a bundle of contact tubes (2). A heat-exchanging medium is guided through the area surrounding the contact tubes. Both ends of the reactor have annular ducts (3,4) with jacket orifices (5,6) for supplying or educting a heat-exchanging medium by means of at least one pump, optionally transferring the heat-exchanging medium or a partial current of the heat-exchanging medium via at least one external heat exchanger. The heat exchanging medium is fed to the lower annular duct (4) and is returned to the pump(s) via the upper annular duct (3). Deviating discs (7) alternately leave open a passage diameter at the centre or at the edge of the reactor. The lower annular duct (4) is split into two zones by means of a horizontal partition (8), said two zones communicating with each other via preferably homogeneously divided openings (9) with adjustable passage diameters.

    Abstract translation: 公开的是（1）具有接触管束（2），围绕通过该接触管的热交换介质循环回路与塞环线路通过一个反应器（3，4）在有夹套的孔的反应器的两端（5,6），用于传热介质的供给和排出 借助于一个或多个泵返回合适的话与所述热交换介质的转移或通过一个或多个外部热交换器中的热交换介质的一个子流，其特征在于，供给到下环形管线的热交换装置（4），并通过所述上部环线（3）（于）泵（一个或多个） 是，并用在反应器中心偏转板（7）交替和离开在反应器边缘，其中，所述下环形管线（4）由水平隔板（8）分成两个区域释放一个通道横截面，彼此（通过优选均匀分布的开口9 ）具有可调节的通道横截面连通。

    COUNTERFLOW REACTOR WITH A BUNDLE OF CONTACT TUBES
    7.
    发明申请
    COUNTERFLOW REACTOR WITH A BUNDLE OF CONTACT TUBES 审中-公开
    具有接触管束的逆流反应器

    公开(公告)号：WO0187476A1

    公开(公告)日：2001-11-22

    申请号：PCT/EP0104975

    申请日：2001-05-03

    Applicant: BASF AG ,  OLBERT GERHARD ,  CORR FRANZ

    Inventor： OLBERT GERHARD ,  CORR FRANZ

    IPC: C07D307/60 ,  B01J19/00 ,  B01J19/24 ,  C07C45/35 ,  C07C47/127 ,  C07C47/22 ,  C07C51/215 ,  C07C51/25 ,  C07C51/265 ,  C07C57/04 ,  C07C57/05 ,  C07D307/89 ,  F28F27/02 ,  C07D401/06 ,  C07D401/12 ,  C07D401/14 ,  C07D405/14

    CPC classification number: C07C51/252 ,  B01J19/0013 ,  B01J19/2425 ,  B01J2219/00094 ,  B01J2219/00103 ,  C07C45/35 ,  C07C47/127 ,  C07C51/215 ,  C07C51/265 ,  F28F27/02 ,  C07C47/22 ,  C07C57/145 ,  C07C57/04 ,  C07C63/16

    Abstract: The invention relates to a reactor (1) comprising a bundle of contact tubes (2). A heat-exchanging medium is guided through the area surrounding the contact tubes. Both ends of the reactor have annular ducts (3,4) with jacket orifices (5,6) for supplying or educting a heat-exchanging medium by means of at least one pump, optionally transferring the heat-exchanging medium or a partial current of the heat-exchanging medium via at least one external heat exchanger. The heat exchanging medium is fed to the lower annular duct (4) and is returned to the pump(s) via the upper annular duct (3). Deviating discs (7) alternately leave open a passage diameter at the centre or at the edge of the reactor. The lower annular duct (4) is split into two zones by means of a horizontal partition (8), said two zones communicating with each other via preferably homogeneously divided openings (9) with adjustable passage diameters.

    Abstract translation: 公开的是（1）具有接触管束（2），围绕通过该接触管的热交换介质循环回路与塞环线路通过一个反应器（3，4）在有夹套的孔的反应器的两端（5,6），用于传热介质的供给和排出 借助于一个或多个泵返回合适的话与所述热交换介质的转移或通过一个或多个外部热交换器中的热交换介质的一个子流，其特征在于，供给到下环形管线的热交换装置（4），并通过所述上部环线（3）（于）泵（一个或多个） 是，并用在反应器中心偏转板（7）交替和离开在反应器边缘，其中，所述下环形管线（4）由水平隔板（8）分成两个区域释放一个通道横截面，彼此（通过优选均匀分布的开口9 ）与可调节的通道横截面进行通信。

    8.
    发明专利
    未知

    公开(公告)号：BRPI0412785B1

    公开(公告)日：2014-11-18

    申请号：BRPI0412785

    申请日：2004-07-21

    Applicant: BASF AG

    Inventor： OLBERT GERHARD ,  HECHLER CLAUS

    IPC: B01J19/32 ,  B01J19/24 ,  C07C45/35 ,  C07C51/215 ,  C07C51/25 ,  C07C57/04 ,  F28D9/00 ,  F28F9/00

    Abstract: The invention relates to a reactor for partial oxidation of a fluid reaction mixture in the presence of a heterogeneous particulate catalyst. Said reactor comprises one or several cuboid heat-transfer sheet modules (1) which are each composed of two or several right-angled heat-transfer sheets (2), arranged parallel to each other such as to form a slit (3) which can be filled with the heterogeneous particulate catalyst and through which the fluid reaction mixture flows, the heat of reaction being absorbed by a heat carrier which flows through the heat-transfer sheets (2) and at least partially evaporates. Said reactor also comprises a mainly cylindrical envelope (4, 15, 16) which depressurizes the heat-transfer sheet modules and fully surrounds said modules, said envelope being composed of a cylinder casing (4) and of caps (15, 16), closing said casing at both ends, the longitudinal axis of which extends parallel to the plane of said heat-transfer sheets (2). Said reactor finally comprises one or several sealing elements (7, 23), arranged so that the fluid reaction mixture flows only through the slit (3), except through the reactor interior spaces, defined by the caps (15, 16).

    REACTOR FOR PARTIAL OXIDATIONS HAVING THERMOPLATE MODULES
    9.
    发明专利
    REACTOR FOR PARTIAL OXIDATIONS HAVING THERMOPLATE MODULES 未知

    公开(公告)号：MY150013A

    公开(公告)日：2013-11-15

    申请号：MYPI20042960

    申请日：2004-07-23

    Applicant: BASF AG

    Inventor： OLBERT GERHARD ,  HECHLER CLAUS DR

    IPC: B01J19/00 ,  B01J19/24 ,  B01J19/32 ,  C07C45/35 ,  C07C51/215 ,  C07C51/25 ,  F28D9/00 ,  F28F9/00

    Abstract: A REACTOR IS PROPOSED FOR PARTIAL OXIDATIONS OF A FLUID REACTION MIXTURE IN THE PRESENCE OF A HETEROGENEOUS PATRICULATE CATALYST, COMPRISING ONE OR MORE CUBOIDAL THERMOPLATE MODULES (1) WHICH ARE EACH FORMED FROM TWO OR MORE RECTANGULAR THERMOPLATES (2) ARRANGED PARALLEL TO EACH OTHER WHILE IN EACH CASE LEAVING A GAP (3) WHICH CAN BE FILLED WITH THE HETEROGENEOUS PARTICULATE CATALYST AND IS FLOWED THROUGH BY THE FLUID REACTION MIXTURE; THE HEAT OF REACTION BEING ABSORBED BY A HEAT CARRIER WHICH FLOWS THROUGH THE THERMOPLATES (2) AND THUS AT LEAST PARTLY EVAPORATES, AND ALSO HAVING A PREDOMINANTLY CYLINDRICAL SHELL (4,15,16) WHICH RELEASES THE PRESSURE AT THE THERMOPLATE MODULES, COMPLETELY SURROUNDS THEM AND COMPRISES A CYLINDER JACKET (4) AND HOODS (15,16) WHICH SEAL IT AT BOTH ENDS AND WHOSE LONGITUDINAL AXIS IS ALIGNED PARALLEL TO THE PLANE OF THE THERMOPLATES (2), AND ALSO HAVING ONE OR MORE SEALING ELEMENTS (7, 23) WHICH ARE ARRANGED IN SUCH A WAY THAT THE FLUID REACTION MIXTURE, APART FROM FLOWING THROUGH THE REACTOR INTERIOR SPACES BOUNDED BY THE HOODS (15,16), ONLY FLOWS THROUGH THE GAP (3).

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